US2271563A - Refrigeration - Google Patents

Refrigeration Download PDF

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US2271563A
US2271563A US317389A US31738940A US2271563A US 2271563 A US2271563 A US 2271563A US 317389 A US317389 A US 317389A US 31738940 A US31738940 A US 31738940A US 2271563 A US2271563 A US 2271563A
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motor
lubricant
boiler
absorber
rotor
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US317389A
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Charles H Macfarland
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Hoover Co
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Hoover Co
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Priority to GB13004/40A priority patent/GB543315A/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/10Sorption machines, plants or systems, operating continuously, e.g. absorption type with inert gas
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Definitions

  • This invention relates to a refrigerating apparatus and control means therefor and more particularly to a three-fluid absorption refrigerating apparatus having power driven means for circulating the mediums in the apparatus with control means for the boiler heating means and ,for the circulating means so constructed that the operation of the circulating means is delayed an appreciable time after the boiler heater is having a motor circulating unit for circulating the mediums in the apparatus in which the oper- I ation of the motor circulating unit is delayed until the boiler is at an operating temperature and to produce this delay'jby submerging the motor rotor in a solid lubricant having a heat of fusion relative to the heating rate of the 'boiler and the heating effect of the motor field such that the motor rotor is blocked until the.
  • absorption refrigerating apparatus of the It is another object of this invention to protype using a motor circulating unit for circulatvid a control for an absorption refrigerating ing an inert medium between the evaporator apparatushavin & motor fan unit fOIWiICHIatand absorber, the solutior between the boiler and ing the mediums in the appa the rotor of absorber and the iiuzrid refrigerant along the which is submerged in a solid lubricant which evaporator, it has been the usual practice to comprises simultaneously energizing the heater start simultaneously the operation of the boiler, for the boiler and the motor, and applying heat and the motor circulating unit. This practice to the motor lubricant to control the period in has the disadvantage that the mediums are bewhich the motor rotor is blocked.
  • the circulationof iumsin the app 1 weak, warm solution from the boiler to the ab- It is another object of this invention to consorber'also has the effect of heatingthe absorber trol the operatio o e m tor by energ zi and thus throwing an additional heat load the motor held and delaying the rotation of the thereon which must be dissipated before the abmotor thereof by means responsive to the ensorber can efiiciently absorb refrigerant.
  • Figure 1 is a diagrammatic view of an absorption refrigerating apparatus using a motor fan circulating unit for circulating the mediums in the apparatus with the control of this invention applied thereto, and
  • Figure 2 is a cross-sectional view of the motor fan unit according to this invention.
  • a three-fluid absorption refrigerating system comprising a boiler B, an analyzer D, an air-cooled rectifier R, a tubular air-cooled vertically positioned condenser C, an evaporator E, a gas heat exchanger H, a tubular air-cooled absorber A, a solution reservoir S, a liquid heat exchanger L and a circulating i'an F which is driven by an electrical motor M.
  • the above described elements are interconnected by various conduits to form a plurality of gas and liquid circuits constituting a complete refrigerating system to which reference will be made in more detail hereinafter.
  • the refrigerating system will be charged with a suitable refrigerant, such as ammonia, a suitable absorbent, such as water, and a suitable inert pressure equalizing medium, such as nitrogen.
  • a suitable refrigerant such as ammonia
  • a suitable absorbent such as water
  • a suitable inert pressure equalizing medium such as nitrogen.
  • the boiler B will be heated in' any suitable manner as by an electric cartridge heater or by a gas burner Ill controlled in a manner to be described later.
  • the application of heat to the boiler B liberates refrigerant vapor from the strong solution therein.
  • the vapor so liberated passes upwardly through an analyzer D in counterflow relationship to a strong solution flowing downwardly through the analyzer.
  • Further refrigerant vapor is generated in the analyzer by the heat of condensation of absorption solution vapor gener ated in the boiler.
  • the refrigerant vapor is conducted from the upper portion of the analyzer D to the upper portion of the condenser through a conduit II which includes the aircooled rectifier R wherein any vapor of absorption solution passing through the analyzer is condensed and returned to the analyzer throu h the conduit l3.
  • the refrigerant vapor is liquefled in the condenser by heat exchange relation with atmospheric air and is discharged from the bottom portion through .a conduit l5 into a downwardly extending conduit I 5.
  • the -bottom portion of the conduit l6 connects with the bottom portion of an upwardly extending conduit ll through a U-bend III.
  • the conduit I8 is longer than the conduit IT for a purpose to be described later.
  • the conduit 11 opens at its upper end into a conduit which discharges into the evaporator in amanner to be more fully described later.
  • the weak. solution formed in the boiler by the generation of rei:.-igerant vapor therefrom is conveyed from the boiler through a conduit 2
  • the weak solution is conveyed from the solution reservoir S through a U-shaped conduit 24 which opens into the gas lift pump 25 which in turn discharges into the upper portion of the absorber A.
  • a small bleed conduit 21 is connected to the discharge conduit 28 of the circulating fan F and opens into the gas lift pump 25 below the solution level normally prevailing in the reservoir whereby the weak solution is elevated into the top of the absorber by gas lift action.
  • the weak solution flows downwardly by gravity in counterflow relation to the rich pressure equalizing medium refrigerant vapor mixture flowing upwardly 'therethrough.
  • the refrigerant vapor content of the mixture is absorbed in the absorption solution and the heat of absorption is conducted to the surrounding air by air cooling fins which are mounted on the exterior of the absorber vessel.
  • the strong solution formed in the absorber flows into a conduit 32 which opens into the inner pass of the liquid heat exchanger L. From the inner pass of the liquid heat exchanger L, the strong solution is conveyed to the upper portion of the analyzer D by a strong solution return pipe 33.
  • the lean pressure equalizing medium refrigerant vapor mixture formed in the absorber A is taken from the upper portion thereof through the conduit 35 into the suction side of the circulating fan F in which it is placed under pressure and discharged through the conduit 28 into the outer pass of the gas heat exchanger H.
  • the pressure equalizing medium under pressure is conveyed from the outer pass of the gas heat exchanger H through a downwardly extending conduit 36 into the bottom portion of the evaporator E.
  • the conduit 20 opens into the bottom portion of. the conduit 36 whereby the liquid refrigerant supplied to the evaporator enters the same simultaneously with the pressure equalizing medium which is placed under pressure by the circulating fan F.
  • the conduit forming the lower part of the evaporator is relatively small whereby the pressure equalizing medium flows through such evaporator conduit with a velocity which is comparatively high.
  • the rapidly flowing pressure equalizing medium sweeps or drags the liq- -uid refrigerant with it through the evaporator into the box cooling portion 40 as the refrigerant is evaporating to produce refrigeration by diifusion into the inert medium.
  • the velocity of the inert gas stream is relatively low by reason of the large diameter of that conduit, and the liquid refrigerant flows therethrough by gravity.
  • the rich pressure equalizing medium refrigerant vapor mixture formed in the evaporator is conducted therefrom into the inner pass of the gas heat exchanger H through a conduit 45.
  • the opposite end of the inner pass of the'gas heat exchanger H communicates with the bottom portion of the absorber A through a conduit 46.
  • the rich pressure equalizing medium refrigerant vapor mixture flows upwardly in counterflow to absorption solution which absorbs the refrigerant vapor content of the mixure.
  • the conduit I6 is made longer than the conduit [1 so as to form a pressure equalizing column of liquid to prevent the pressure built up by the fan F from being blown back through the condenser C.
  • the bottom coil of the evaporator E is provided with a drain conduit 48 which opens into the strong solution return conduit 32.
  • the conduit 48 opens into the top portion of the evaporator coil whereby it will not completely drain such conduit.
  • the discharge conduit l of the condenser is vented through a vent conduit 49 into the inner pass of the gas heat exchanger H.
  • the bleed conduit 21 which leads'to the gas lift pump is so connected to the discharge conduit 28 of the fan F that. any liquid mediums condensed in the outer pass of the heat exchanger H and conduit 28 will be conducted back to the solution circuit and thus not interfere with the operation of the motor-fan unit.
  • is positioned against the coils of the evaporator E and connected by a tube 52 to a control device 53.
  • One side of the control device 53 is connected by a conductor 54 to one side of the power line.
  • the opposite side of the control device 53 is connected by conductor 59 to a magnetically operated gas valve 55 and by conductor 56 to one side of the motor field coils.
  • the opposite side of the motor field coils and the magnetic valve 55 is connected by conductors 51 and 58 to the opposite side of the power line.
  • a low flame by-pass may be pro,- vided, by-passing the valve 55 to provide a mini-
  • the lubricant selected should be chemically inert; it should not be volatile at normal temperature; it should be solid or non-fluid at normal temperature or indisplaceable so that it will not get out of the motor during shipment;
  • One such lubricant is paraflin and it is obtainable in along range of melting points and specific gravity. By selecting parafiln of the proper melting point or by mixing it with other lubricants,
  • a lubricant By mixing parafiin with other well known high specific gravity lubricants, a lubricant can be obtained which has a specific gravity greater than ,1.0 so that it will not be displaceable by the liquid mediums in the apparatus, which lubricant will be in a solid state at normal temperature so that it will not get out of the motor during shipment and which will be fluid at the operating temperature of the motor to provide for proper lubrication of the motor without materially retarding the rotation of the rotor.
  • the rotor centers itself as it reaches its operating speed. This is due to the fact that if the rotor is of! center at the beginning of its operation, the liquid will tend to rotate with the rotor and be drawn between the rotor mum flame to the burner Ill during idle periods.
  • the rotor 62 is rigidly connected to the fan F by a shaft 64 which is rotatably supported on the interior of the casing by bearing assemblies 65 and 66.
  • the lower bearing assembly includes a two part thrust bearing II of very hard material such as tungsten carbide and a large clearance Babbitt radial bearing 12.
  • the top bearing assembly 66 also includes a large clearance Babbitt radial bearing 13.
  • the shaft 64 is preferably made of stainless steel.
  • annular upstanding wall 61 Formed as a part of the bearing assembly '65 is an annular upstanding wall 61 surrounded by a throw-off ring 68 formed as a part of the fan 1 F.
  • the upstanding wall 61 extends above the bottom of outlet conduit 26 so as to form a drain for the fan housing.
  • the fan housing is divided into a suction chamber and a high pressure chamber by late 69 having an aperture HI lead- 62 and shell 6
  • buoyant effect of the lubricant or other liquid will also lighten the load on the thrust bearing H and thereby reduce the wear thereon. Since the radial bearings are out of contact with the shaft during operation a much quieter motor will result.
  • the heating effect of the motor field may remain fixed and the melting point of the lubricant be varied or the melting point of the lubricant be selected and the heating effect of the field be varied to predetermine the time interval the rotor remains blocked.
  • the melting point of the lubricant should be so selected relative to the heating rate of the boiler and the heating effect of the motor field thatthe lubricant will be melted by the time the boiler has come up to operating temperature.
  • the absorption solution is not being circulated until the boiler reaches an operative temperature, the cold solution from the absorber will not operate to cool the boiler and thereby the boiler will come up to a proper operative temperature sooner than it would if the motor fan is operated simultaneously with the heater.
  • the warm inert medium will not be circulated from the absorber to the evaporator and therefore the evaporator will remain in its cold state until refrigeration isbeing produced therein.
  • the motor fan unit is fabricated, filled to the desired level with fused lubricant, and suitably secured to the remainder of the apparatus.
  • the lubricant then congeals and the system is charged in the usual manner. It can thus be seen that the refrigerating apparatus can be shipped and otherwise handled and the lubricant will remain in the motor shell.
  • the motor shell When the apparatus is in operating position the motor shell will and which is not displaceable by the liquid meill diums in the system, and which cannot get out of the motor shell during shipment.
  • this invention provides an absorption refrigerating apparatus having a motor circulator unit in which the operation of the motor circulator unit is delayed until the boiler is up to an operating temperature and in which the delay is accomplished or controlled in part by the heating effect of the motor field and in part by the heat of fusion of the lubricant selected.
  • That process of controlling the operation of a continuous absorption refrigerating apparatus of the type using a pressure equalizing medium and having heating means for the boiler and power operated means for circulating the inert medium comprising simuiltaneously energizirig the heating means and power operated means and applying a retarding influence to the operation of said power operated means.
  • the method of controlling the operation of an absorption refrigerating apparatus of the type having a heater for the boiler and an electro-magnetic circulator unit for circulating the mediums within the system comprisingenergizing the apparatus, delaying the operation of the circulator unit and terminating the delaying step by heat generated by the energy supplied to the apparatus.
  • An absorption refrigerating apparatus comprising a boiler, an evaporator and an absorber
  • conduits connecting-said evaporator and absorber to form a'circuit therebetween conduits connecting said boiler and absorber to form a circuit therebetween, a heater for said boiler, power,
  • An absorption refrigerating apparatus comprising a boiler, a condenser, an evaporator and an absorber, conduits connecting said evaporator and absorber to form a circuit therebetween, conduits connecting said boiler and absorber to form a circuit therebetween, a conduit leading from said condenser to said evaporator, the top of said evaporator being positioned above the bottom of said condenser, power operated means in said circuit between the evaporator and absorber for circulating an inert pressure equalizing medium in its circuit, conduit means connecting said power operated means with the circuit between the boiler and absorber, and being so arranged relative'thereto that pressure developed by said power means will circulate a solvent between the boiler and absorber, said circuit between the evaporator and absorber being so arranged relative to the conduit leading from the condenser to the evaporator that pressure developed by said power means will circulate condensed refrigerant along the evaporator, a heater for said boiler and control means for simultaneously energizing the heater
  • control means for simultaneously energizing the motor and heater, heat responsive means for-blocking the motor rotor, said heat responsive means being subject to heat generated by the motor and operative to release the motor rotor a predjetermined period after the mo-.
  • tor is energized w ereby the motor fan unit will be operative to circulate the mediums in the ap-' operative the boiler, control means for simultaneously en-,
  • a field structure In an electric motor, a field structure, a rotor, means for energizing the field structure and means for retarding the rotation of the rotor, said means being constructed to release its retardation of the rotor after a predetermined interval.
  • An absorption refrigerating apparatus comprising a boiler, a condenser, an evaporator and an absorber, conduits connected to said evaporator and absorber to form an inert gas circuit between said evaporator and absorber, said apparatus being charged with a refrigerant, a liquid absorbent and an inert gas, and power operated means in said closed circuit for circulating the inert gas in said circuit, said power operated means comprising a motor rotor and fan in which the motor rotor is submerged in a lubricant, and said power operated means being positioned in a part of said inert gas circuit inaccessible to the liquid medium within the apparatus under normal operating conditions.
  • An absorption refrigeratingapparatus comprising a boiler, an evaporator and an absorber, conduits connecting said evaporator and absorber to form an inert gas circuit therebetween, conduits connecting the boiler and absorber to form a solution circuit therebetween, said apparatus being charged with a refrigerant, a liquid absorbent and an inert gas, power operated means in said evaporator-absorber circuit for circulating an inert gas in'said circuit, said power operated means comprising a motor rotor and fan enclosed in a casing and in which the motor rotor is submerged in a lubricant, and a conduit leading from the discharge side of said fan to the boiler-absorber circuit and so related thereto as to circulate absorption solution in said circuit, said motor fan casing being positioned in a part of said evaporator-absorber circuit normally inaccessible to liquid mediums in the apparatus but subject to being flooded during idle periods, said conduit leading from the discharge side of the 7 fan to the boiler-absor
  • An absorption refrigerating apparatus comprising a boiler, an evaporator and an absorber, conduits connecting said evaporator and absorber to form an inert gas circuit therebetween, said apparatus being charged with a refrigerant, a liquid absorbent and an inert gas, power operated means in said circuit between the evaporator and absorber for circulating the inert gas in its circuit, said power operated means comprising a motor fan unit in which the motor rotor is submerged in a lubricant and is positioned in a the evaporator and absorber that any accumulated liquid medium will drain away from the fan unit during idle periods whereby the lubricant in the motor housing will not be diluted by the liquid mediums within the system.
  • An absorption refrigerating apparatus of the type having a motor fan unit for circulating an inert medium in a circuit between the evaporator and absorber and which is also charged with liquid mediums, in which the motor ian unit positioned in a part of the circuit normally inaccessible to the liquid mediums in the apparatus but subject to being flooded with the liquid medium when the apparatus is tipped and in which the motor rotor is submerged in a lubricant which is solid at ordinary temperatures.
  • An absorption refrigerating apparatus in cluding a motor driven medium circulator, said motor driven medium circulator including a motor rotor submerged in a lubricant and said apparatus being charged with a refrigerant and a' solvent, said lubricant being indisplaceable by the refrigerant or the solvent.
  • An absorption refrigerating apparatus including a motor fan unit for circulating the mediums in the apparatus, said motor fan unit having the motor rotor submerged in a lubricant and said apparatus being charged with a refrigerant and a solvent therefor, said motor fan unit being positioned in a part of the apparatus normally inaccessible to the liquid mediums in the apparatus but subject to be flooded thereby when theapparatus is tipped, said lubricant being indisplaceable by the liquid mediums in the apparatus.
  • An absorption refrigerating apparatus comprising an inert gas circuit and a solution circuit, a motor circulator unit for circulating a medium in one of said circuits, said circulator unit including a rotor submerged in a solid lubricant.
  • An absorption refrigerating apparatus of the type having liquid and gaseous mediums therein and closed circuits for said mediums, in combination with a circulator unit for at least one 'of said mediums hermetically sealed within the walls of the apparatus, said circulator unit including a motor rotor and fan, said motor rotor being submerged in a lubricant and positioned outside said circuits.
  • An absorption refrigerating apparatus comprising an evaporator and an absorber, conduits connecting said evaporator and absorber to form an inert gas circuit therebetween, said apparatus being charged with a refrigerant, an absorbent,
  • saidpower operated means comprising a' motor fan rotor in which the motor rotor is submerged in a lubricant non-fluid at ordinary temperatures.
  • An absorption refrigerating apparatus of the type having a motor fan unit for circulating an inert medium in a circuit between the evaporator and absorber, said motor comprising a vertically extending casing having an upper fan casing and a lower shell, a motor rotor in said shell and a motor field outside said shell supporting it against internal pressure, said shell containing a. solid lubricant.
  • An absorption refrigerating apparatus including a heater for the boiler and a motor fan unit for circulating the mediums in the apparatus in which the motor fan rotor is submerged in the lubricant solid at ordinary temperatures but fusible at higher temperatures, said, lubricant having a heat of fusion of such value and being present in such amount relative to the heating rate of the boiler and the power input to the motor that the heat of the motor will fuse the lubricant by the time the heater has brought the boiler to operating temperatures when the heater and motor are simultaneously energized.
  • That improvement in the art of refrigeration which comprises lubricating the moving parts of a refrigerating apparatus by means of a lubricant which is non-fluid at ordinary temperatures and liquid at the operating temperature of the apparatus, whereby the lubricant cannot be displaced by the refrigerating medium during inoperative periods.
  • That improvement in the art of lubricating motors which comprises submerging the motor rotor in a lubricant which is non-fluid at ordinary temperatures but fluid at the operating temperature of the motor.
  • a fractional horse power motor fan unit for circulating an inert medium in an absorption refrigerating apparatus comprising a ver-- tically extending hermetically sealed casing and a motor fan rotor rotatably mounted in said casing, said motor rotor being submerged in a lubricant solid at ordinary temperatures but fusible at higher temperatures.
  • a fractional horse power motor fan unit for circulating an inert medium in an absorption refrigerating apparatus comprising a vertically extending hermetically sealed casing, a motor fan rotor rotatably mounted in said casing, and a field structure externally of said casing, said motor rotor being submerged in a lubrica'nt, said lubricant being of such nature that it fuses due to the heat generated by said field structure.
  • a motor comprising a casing and a rotor mounted in said casing, said casing containing a lubricant solid at ordinary temperatures but fusible at higher temperatures.
  • That improvement in the art of refrigeration in which a power driven circulator is used to circulate the medium which comprises, charging a refrigerating apparatus with a liquid working medium, charging a fused lubricant into the apparatus in a position to surround the moving parts of the circulator, allowing the lubricant to congeal and re-fusing the lubricant prior to operation whereby the lubricant cannot be displaced by the liquid working medium during shipment or other inoperative periods and is in a condition to lubricate the moving parts of the circulator during operation.
  • an absorption refrigerating apparatus of the type having liquid and gaseous mediums therein and closed circuits for said mediums in combination with a circulator unit for at least one of said mediums, said circulator unit including a movable element located in a closed casing hermetically sealed to, in open communication with and extending from one of said circuits so as to be outside the path of flow of the medium being circulated in said circuit and a lubricant in said casing having a specific gravity higher than the medium being circulated in said circuit whereby the movable element wll be lubricated and the lubricant will not be carried along with the circulating medium to other parts of the apparatus.
  • an absorption refrigerating apparatus including a closed inert gas circuit and means for circulating an inert gas in said circuit, said means including a movable element in a closed casing hermetically sealed to, in open communication with and extending from said circuit so as to be out of the path of flow of the inert gas in said circuit and said casing containing a lubricant whereby said movable element will be lubricated and the lubricant will not be entrained in the circulating inert gas and be carried to the other parts of the apparatus.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Motor Or Generator Frames (AREA)
  • Motor Or Generator Cooling System (AREA)
  • Sorption Type Refrigeration Machines (AREA)

Description

Patented Feb. 3, 1942 2,271,563 REFRIGERATION Charles H. MacFarland, Springfield, Mass., as-
signor to The Hoover Company, North Canton, Ohio, a corporation of Ohio Application February 5, 1940, Serial No. 317,389
40 Claims.
This invention relates to a refrigerating apparatus and control means therefor and more particularly to a three-fluid absorption refrigerating apparatus having power driven means for circulating the mediums in the apparatus with control means for the boiler heating means and ,for the circulating means so constructed that the operation of the circulating means is delayed an appreciable time after the boiler heater is having a motor circulating unit for circulating the mediums in the apparatus in which the oper- I ation of the motor circulating unit is delayed until the boiler is at an operating temperature and to produce this delay'jby submerging the motor rotor in a solid lubricant having a heat of fusion relative to the heating rate of the 'boiler and the heating effect of the motor field such that the motor rotor is blocked until the.
energized. p boiler reaches an operating temperature;
In absorption refrigerating apparatus of the It is another object of this invention to protype using a motor circulating unit for circulatvid a control for an absorption refrigerating ing an inert medium between the evaporator apparatushavin & motor fan unit fOIWiICHIatand absorber, the solutior between the boiler and ing the mediums in the appa the rotor of absorber and the iiuzrid refrigerant along the which is submerged in a solid lubricant which evaporator, it has been the usual practice to comprises simultaneously energizing the heater start simultaneously the operation of the boiler, for the boiler and the motor, and applying heat and the motor circulating unit. This practice to the motor lubricant to control the period in has the disadvantage that the mediums are bewhich the motor rotor is blocked.
- ing circulated before the boiler is at an operat- 2o In a s ption refr e a appa a us f t ing temperature resulting in a decreased eiiitype us pow means circulating the ciency since no refrigeration can be produced. diums in the apparatus, it is essential that the until the boiler has reached its operating temparts of the motor be protected from the Corroperature to distill ofi refrigerant .vapor for consive action of the refri densation in the condenser. It is therefore another object of this invention The circulation of the cold solution from the to place the motor fan unit in that p 1 the absorber to the boiler also has the effect of coolcirculating Sy t n rmally inaccessible to liqing the boiler and this further delays the starting uid mediums and to immerse the rotor in a lubritime since the heater must also heat this cool cant whereby the motor parts a e p otec ed from solution before the boiler reaches its operating e c rrosive action of the refrigerant and the temperature, thus reducing the operating eflilubricant cannot be diluted by the liquid mediciency of the apparatus. The circulationof iumsin the app 1 weak, warm solution from the boiler to the ab- It is another object of this invention to consorber'also has the effect of heatingthe absorber trol the operatio o e m tor by energ zi and thus throwing an additional heat load the motor held and delaying the rotation of the thereon which must be dissipated before the abmotor thereof by means responsive to the ensorber can efiiciently absorb refrigerant. vapor ergy of the motor held and, more particularly, in from the inert medium refrigerant vapor mixwhich the energy responsive means is a lubricant tune circulating e ough. Since the inert non-fluid at ordinary temperature and fluid at medium being circulated at this time contains 40 the operating temperatures of the motor. little refrigerant vapor to be absorbed, the soluv In absorption refrigerating apparatus using a tion leaving the absorber and returning to the motor fan circulating unit, it is necessary that. boiler will be comparatively weak which will rethe lubricant be retained in the motor shell both suit in a further decrease in the efllciency of the during shipment and at other. idle periods. apparatus' a It is therefore another object of this invention The circulation of warm inert medium from o Provide an absorption refrigerating apparatus the absorber to the evaporator acts to heat the in which e lubricant the moving parts evaporator before any liquid refrigerant is prothereof s n displaooable y the q d ediduced to cool it by the evaporation of the refrigums in the appara us y ea of being onerant. The apparatus thus operates to pump uid at Ce tai t mes or by being heavier than heat from the boiler to the evaporator and furthe liquids in the appara ereby the refrigther reduce the efficiency of the apparatus. erating apparatus can be tipped without. losing It is therefore an object of this invention to the oil from the motor fan unit and is retained provide an absorption refrigerating apparatus 5 in its normal position at other times.
i It is also an object of this invention to provide an improved motor fan for circulating the medium in an absorption refrigerating apparatus in which the rotor is positioned in the interior of the apparatus and submerged in a solid lubricant and the stator is positioned outside the system walls.
Other objects and advantages of this invention will become apparatus as the description proceedswhen taken in connection with the accompanying drawing in which:
Figure 1 is a diagrammatic view of an absorption refrigerating apparatus using a motor fan circulating unit for circulating the mediums in the apparatus with the control of this invention applied thereto, and
Figure 2 is a cross-sectional view of the motor fan unit according to this invention.
Referring to Figure 1 of the drawing, there is disclosed a three-fluid absorption refrigerating system comprising a boiler B, an analyzer D, an air-cooled rectifier R, a tubular air-cooled vertically positioned condenser C, an evaporator E, a gas heat exchanger H, a tubular air-cooled absorber A, a solution reservoir S, a liquid heat exchanger L and a circulating i'an F which is driven by an electrical motor M. The above described elements are interconnected by various conduits to form a plurality of gas and liquid circuits constituting a complete refrigerating system to which reference will be made in more detail hereinafter.
The refrigerating system will be charged with a suitable refrigerant, such as ammonia, a suitable absorbent, such as water, and a suitable inert pressure equalizing medium, such as nitrogen.
The boiler B will be heated in' any suitable manner as by an electric cartridge heater or by a gas burner Ill controlled in a manner to be described later.
The application of heat to the boiler B liberates refrigerant vapor from the strong solution therein. The vapor so liberated passes upwardly through an analyzer D in counterflow relationship to a strong solution flowing downwardly through the analyzer. Further refrigerant vapor is generated in the analyzer by the heat of condensation of absorption solution vapor gener ated in the boiler. The refrigerant vapor is conducted from the upper portion of the analyzer D to the upper portion of the condenser through a conduit II which includes the aircooled rectifier R wherein any vapor of absorption solution passing through the analyzer is condensed and returned to the analyzer throu h the conduit l3. The refrigerant vapor is liquefled in the condenser by heat exchange relation with atmospheric air and is discharged from the bottom portion through .a conduit l5 into a downwardly extending conduit I 5. The -bottom portion of the conduit l6 connects with the bottom portion of an upwardly extending conduit ll through a U-bend III. The conduit I8 is longer than the conduit IT for a purpose to be described later. The conduit 11 opens at its upper end into a conduit which discharges into the evaporator in amanner to be more fully described later.
The weak. solution formed in the boiler by the generation of rei:.-igerant vapor therefrom is conveyed from the boiler through a conduit 2|, the outer pass of liquid heat exchanger L, an
air-cooled pre cooler and a conduit 23 into the solution reservoir S. The weak solution is conveyed from the solution reservoir S through a U-shaped conduit 24 which opens into the gas lift pump 25 which in turn discharges into the upper portion of the absorber A. It is apparent that the top of absorber A is materially above the solution level normally prevailing in the boiler-analyzer reservoir system whereby some means must be provided to elevate the absorption solution into the top of the absorber A. For this purpose a small bleed conduit 21 is connected to the discharge conduit 28 of the circulating fan F and opens into the gas lift pump 25 below the solution level normally prevailing in the reservoir whereby the weak solution is elevated into the top of the absorber by gas lift action.
In the absorber, the weak solution flows downwardly by gravity in counterflow relation to the rich pressure equalizing medium refrigerant vapor mixture flowing upwardly 'therethrough. The refrigerant vapor content of the mixture is absorbed in the absorption solution and the heat of absorption is conducted to the surrounding air by air cooling fins which are mounted on the exterior of the absorber vessel. The strong solution formed in the absorber flows into a conduit 32 which opens into the inner pass of the liquid heat exchanger L. From the inner pass of the liquid heat exchanger L, the strong solution is conveyed to the upper portion of the analyzer D by a strong solution return pipe 33.
The lean pressure equalizing medium refrigerant vapor mixture formed in the absorber A is taken from the upper portion thereof through the conduit 35 into the suction side of the circulating fan F in which it is placed under pressure and discharged through the conduit 28 into the outer pass of the gas heat exchanger H. The pressure equalizing medium under pressure is conveyed from the outer pass of the gas heat exchanger H through a downwardly extending conduit 36 into the bottom portion of the evaporator E.
The conduit 20 opens into the bottom portion of. the conduit 36 whereby the liquid refrigerant supplied to the evaporator enters the same simultaneously with the pressure equalizing medium which is placed under pressure by the circulating fan F. The conduit forming the lower part of the evaporator is relatively small whereby the pressure equalizing medium flows through such evaporator conduit with a velocity which is comparatively high. The rapidly flowing pressure equalizing medium sweeps or drags the liq- -uid refrigerant with it through the evaporator into the box cooling portion 40 as the refrigerant is evaporating to produce refrigeration by diifusion into the inert medium. In the con duit 40 the velocity of the inert gas stream is relatively low by reason of the large diameter of that conduit, and the liquid refrigerant flows therethrough by gravity.
'The rich pressure equalizing medium refrigerant vapor mixture formed in the evaporator is conducted therefrom into the inner pass of the gas heat exchanger H through a conduit 45. The opposite end of the inner pass of the'gas heat exchanger H communicates with the bottom portion of the absorber A through a conduit 46. In the absorber A, the rich pressure equalizing medium refrigerant vapor mixture flows upwardly in counterflow to absorption solution which absorbs the refrigerant vapor content of the mixure.
Any refrigerant unevaporated in the evaporator E will flow through the conduit 45, the inner 46 to the bottom of the absorber.
pass of the gasheat exchanger H and conduit Since the motor fan unit is in the opposite part of the pressureequalizing medium circuit, this unevaporated refrigerant cannot reach the motor fan unit and interfere with its operation.
The conduit I6 is made longer than the conduit [1 so as to form a pressure equalizing column of liquid to prevent the pressure built up by the fan F from being blown back through the condenser C.
The bottom coil of the evaporator E is provided with a drain conduit 48 which opens into the strong solution return conduit 32. The conduit 48 opens into the top portion of the evaporator coil whereby it will not completely drain such conduit.
The discharge conduit l of the condenser is vented through a vent conduit 49 into the inner pass of the gas heat exchanger H. The solution reservoir Sis vented through a conduit 50 into the suction conduit 35 of the circulating fan.
The bleed conduit 21 which leads'to the gas lift pump is so connected to the discharge conduit 28 of the fan F that. any liquid mediums condensed in the outer pass of the heat exchanger H and conduit 28 will be conducted back to the solution circuit and thus not interfere with the operation of the motor-fan unit.
A thermostatic bulb 5| is positioned against the coils of the evaporator E and connected by a tube 52 to a control device 53. One side of the control device 53 is connected by a conductor 54 to one side of the power line. The opposite side of the control device 53 is connected by conductor 59 to a magnetically operated gas valve 55 and by conductor 56 to one side of the motor field coils. The opposite side of the motor field coils and the magnetic valve 55 is connected by conductors 51 and 58 to the opposite side of the power line. A low flame by-pass may be pro,- vided, by-passing the valve 55 to provide a mini- The lubricant selected should be chemically inert; it should not be volatile at normal temperature; it should be solid or non-fluid at normal temperature or indisplaceable so that it will not get out of the motor during shipment;
'it should be fluid and have a low viscosity at the operating temperature of the motor; it should not be miscible with water and it should have good lubricating properties.
One such lubricant is paraflin and it is obtainable in along range of melting points and specific gravity. By selecting parafiln of the proper melting point or by mixing it with other lubricants,
almost any melting point desired can be obtained.
By mixing parafiin with other well known high specific gravity lubricants, a lubricant can be obtained which has a specific gravity greater than ,1.0 so that it will not be displaceable by the liquid mediums in the apparatus, which lubricant will be in a solid state at normal temperature so that it will not get out of the motor during shipment and which will be fluid at the operating temperature of the motor to provide for proper lubrication of the motor without materially retarding the rotation of the rotor. v
By submerging the rotor 62 in a liquid medium such as a lubricant, the rotor centers itself as it reaches its operating speed. This is due to the fact that if the rotor is of! center at the beginning of its operation, the liquid will tend to rotate with the rotor and be drawn between the rotor mum flame to the burner Ill during idle periods.
' and is supported against internal pressure by the stator 63' being pressed tightly thereover. The rotor 62 is rigidly connected to the fan F by a shaft 64 which is rotatably supported on the interior of the casing by bearing assemblies 65 and 66. The lower bearing assembly includes a two part thrust bearing II of very hard material such as tungsten carbide and a large clearance Babbitt radial bearing 12. The top bearing assembly 66 also includes a large clearance Babbitt radial bearing 13. The shaft 64 is preferably made of stainless steel.
Formed as a part of the bearing assembly '65 is an annular upstanding wall 61 surrounded by a throw-off ring 68 formed as a part of the fan 1 F. The upstanding wall 61 extends above the bottom of outlet conduit 26 so as to form a drain for the fan housing. The fan housing is divided into a suction chamber and a high pressure chamber by late 69 having an aperture HI lead- 62 and shell 6| at the point where the rotor is closest to the shell and move the rotor away from the'shell at that point. This action will continue until the rotor is completely centralized. It is to be noted that the space between the rotor and shell when the rotor is centered is very small and may be only a few thousandths of an inch.
The fact that the action of the lubricant automatically centers the rotor renders it possible to make the radial Babbitt bearings I2 and 13 with a much larger clearance between their bearing surfaces and that of the shaft 64 than would otherwise be possible. Thus the bearing surfaces are only in contact when the rotor is starting and the wear thereon will be negligible.
The buoyant effect of the lubricant or other liquid will also lighten the load on the thrust bearing H and thereby reduce the wear thereon. Since the radial bearings are out of contact with the shaft during operation a much quieter motor will result.
When the system shuts down the lubricant in the shell 6| will solidify. Now if the machine calls for refrigeration, the control 53 willsimultaneously energize themagnetic valve 56 to supply gas to the burner, II and also energize the field coils of the motor. The motor rotor, being blocked by the solid lubricant, cannot operate to rotate the fan F and therefore no inert pressure equalizing medium will be circulated in its circuit with the result that the gas lift pump 25 will not operate to circulate the solution between the boiler and absorber, nor will any liquid re? frigerant be circulated through the evaporator E. The heating effect of the motor field may remain fixed and the melting point of the lubricant be varied or the melting point of the lubricant be selected and the heating effect of the field be varied to predetermine the time interval the rotor remains blocked. The melting point of the lubricant should be so selected relative to the heating rate of the boiler and the heating effect of the motor field thatthe lubricant will be melted by the time the boiler has come up to operating temperature.
If a lubricant having the proper melting point is selected, relative to the heating rate of the boiler and the heating effect of the motor field, the motor fan unit will remain blocked until the boiler has reached an operating temperature, at
which time liquid refrigerant will be supplied as not to interfere with the operation of the motor fan unit. At the same time a portion of the inert medium will flow through tube 21 to gas lift pump 25 and thereby circulate the absorption solution between the boiler and absorber as previously described.
Since the absorption solution is not being circulated until the boiler reaches an operative temperature, the cold solution from the absorber will not operate to cool the boiler and thereby the boiler will come up to a proper operative temperature sooner than it would if the motor fan is operated simultaneously with the heater. The warm inert medium will not be circulated from the absorber to the evaporator and therefore the evaporator will remain in its cold state until refrigeration isbeing produced therein.
Any liquid medium which may condense in the outer pass of the gas heat exchanger H and conduit 28 will be collected in the bottom thereof and cannot flow into the motor fan unit. Any liquid which condenses in the fan casing ill will be thrown off by the throw-off ring 68 before it can enter the motor shell BI and dilute the lubricant. The condensed mediums which may collect in the bottom of the gas heat exchanger will flow through the. bleed conduit 21 back to the solution circuit. When the machine begins opera-,-
tion again, the liquid medium in the fan casing will soon be evaporated by diffusion into the inert pressure equalizing medium flowing to the gas heat exchanger and therefore cannot accumulate so as to interfere with the operation of the motor fan unit. Since the wall 61 is above the bottom of outlet 28 no liquid medium can enter the motor shell and dilute or displace the lubricant therein.
The motor fan unit is fabricated, filled to the desired level with fused lubricant, and suitably secured to the remainder of the apparatus. The lubricant then congeals and the system is charged in the usual manner. It can thus be seen that the refrigerating apparatus can be shipped and otherwise handled and the lubricant will remain in the motor shell. When the apparatus is in operating position the motor shell will and which is not displaceable by the liquid meill diums in the system, and which cannot get out of the motor shell during shipment.
It can also be seen that this invention provides an absorption refrigerating apparatus having a motor circulator unit in which the operation of the motor circulator unit is delayed until the boiler is up to an operating temperature and in which the delay is accomplished or controlled in part by the heating effect of the motor field and in part by the heat of fusion of the lubricant selected.
While I have shown my invention positioned in the'inert gas circuit of a three-fluid refrigerating apparatus, it is obvious that it could be placed in the solution circuit of either a two or three-fluid refrigerating apparatus for circulating the solution alone.
While I have shown but one embodiment of my invention, it is to be understood that this embodiment is to be taken as illustrative only and not in a. limiting sense. I do not wish to be limited to the particular structure shown and described but to include all equivalent variations thereof except as limited by the claims.
I claim:
1. That process of controlling the operation of a continuous absorption refrigerating apparatus of the type using a pressure equalizing medium and having heating means for the boiler and power operated means for circulating the inert medium comprising simuiltaneously energizirig the heating means and power operated means and applying a retarding influence to the operation of said power operated means.
2. That method of operating an absorption refrigerating apparatus having a heater and means for circulating the mediums in the apparatus in which the medium circulating means includes a motor in which the rotor is submerged in a congealed lubricant which comprises simultaneously energizing the heater and medium circulating means 8; cl utilizing the heat of fusion.
of the lubricant o delay the operation of the medium circulating means.
3. The method of controlling the operation of an absorption refrigerating apparatus having a heater and a motor fan unit for circulating the mediums therein in which the motor rotor is submerged in a lubricant solid-at ordinary temperatures but fusible at higher temperatures which comprises simultaneously energizing the heater and motor and utilizing the time interval necessary for the heat of the motor to fuse the lubricant for delaying the operation of the motor fan unit.
4. The method of controlling the operation of an absorption refrigerating apparatus of the type having a heater for the boiler and a motor fan circulator unit for circulating the mediums in the apparatus in which the motor rotor is submerged in a lubricant which is non-fluid at ordinary temperatures but which is fluid under the operating conditions of the motor comprising slmultaneously energizing the heater and the motor and heating the lubricant to melt the same.
5. The method of controlling an absorption refrigerating apparatus of the type having a motor fan unit for circulating the mediums in the apparatus and having the motor rotor thereof submerged in a non-fluid lubricant and a heater for the boiler comprising simultaneously energizing the motor and the heater, utilizing the non-fluid lubricant to block the rotor until the boiler comes up to an operating temperature and utilizing the energy supplied tothe motor to melt the lubricant whereby the motor fan unit becomes operative to circulate the mediums in the apparatus when the boiler reaches an operating temperature. I
6. The method of controlling an absorption refrigerating apparatus of the type having a heater for the boiler and means for circulating an inert medium between the evaporator and absorber, a refrigerant solvent between the boiler and absorber and for circulating liquid refrigerant along the evaporator comprising simultaneously energizing the heater and circulating means responsive to a demand for refrigeration and delaying the circulation of the inert medium, solvent and liquid refrigerant until the boilerhas reached an operating temperature.
'7. The method of controlling the operation of an absorption refrigerating apparatus of the type having a heater for the boiler and an electro-magnetic circulator unit for circulating the mediums within the system comprisingenergizing the apparatus, delaying the operation of the circulator unit and terminating the delaying step by heat generated by the energy supplied to the apparatus.
8. The method of controlling the operation of an absorption refrigerating apparatus of the type having a heater for the'boiler and an electric motor fan unit for circulating the mediums in the apparatus comprising simultaneously energizing the heater and motor fan unit, delaying the operation of the motor fan unit by blocking its rotor and terminating the delaying step by the energy supplied to the circulator unit.
9. The method of controlling the operation of an absorption refrigerating apparatus of the type having a heater for the boiler and a motor-fan unit for circulating the mediums in the apparatus comprising simultaneously energizing the heater and the motor-fan unit, delaying the operation of the motor fan unit by blocking the motor rotor with a lubricant solid at ordinary temperatures but fusible at higher temperatures and terminating the delay step by the heat of fusion of the lubricant and the energy supplied to the motor fan unittodetermine the period the rotor remains blocked.
10. The method of controlling the operation of an absorption refrigerating apparatus of the type having an electro-magnetic circulator unit for circulating the. mediums in the apparatus comprising energizing the circulator unit, delaying the operation of the circulator unit and utilizing the energy supplied to the circulator unit to govern the period or delay.
11. An absorption refrigerating apparatus comprising a boiler, an evaporator and an absorber,
conduits connecting-said evaporator and absorber to form a'circuit therebetween, conduits connecting said boiler and absorber to form a circuit therebetween, a heater for said boiler, power,
operated means in said first-mentioned circuit for circulating an inert pressure equalizing medium in its circuit, a conduit leading from said power operated means to said second-mentioned .circuit, and being so arranged therewith as to cirmerged in a lubricant which is solid at ordinary temperatures but fusible at higher temperatures and is present in such amounts that the circulation of the inert medium and solvent is delayed until the boiler is at an operating temperature.
12. An absorption refrigerating apparatus comprising a boiler, a condenser, an evaporator and an absorber, conduits connecting said evaporator and absorber to form a circuit therebetween, conduits connecting said boiler and absorber to form a circuit therebetween, a conduit leading from said condenser to said evaporator, the top of said evaporator being positioned above the bottom of said condenser, power operated means in said circuit between the evaporator and absorber for circulating an inert pressure equalizing medium in its circuit, conduit means connecting said power operated means with the circuit between the boiler and absorber, and being so arranged relative'thereto that pressure developed by said power means will circulate a solvent between the boiler and absorber, said circuit between the evaporator and absorber being so arranged relative to the conduit leading from the condenser to the evaporator that pressure developed by said power means will circulate condensed refrigerant along the evaporator, a heater for said boiler and control means for simultaneously energizing the heater and power operated means, said power operated means comprising a motor fan unit in which the motor rotor is submerged in a lubricant solid at ordinary temperatures but fusible at higher temperatures and is present in such amountsthat the circulation of' inert medium, solvent, and liquid refrigerant is delayed until the boiler is at an operating temperature.
13. In an absorption refrigerating apparatus of the type having a motor fan unit for circulating the mediums in the apparatus and a heater for the boiler, control means for simultaneously energizing the motor and heater, heat responsive means for-blocking the motor rotor, said heat responsive means being subject to heat generated by the motor and operative to release the motor rotor a predjetermined period after the mo-.
tor is energized w ereby the motor fan unit will be operative to circulate the mediums in the ap-' operative the boiler, control means for simultaneously en-,
ergiz ing the motor and the heater, means associated with the motor for blocking the motor rotor, said means being responsive to the energy supplied to the motor and operative to release the motor a predetermined period after the motor is energized, whereby the motor fan unit will be operative to circulate the mediums in the apparatus when the boiler reaches an operative temperature.
15. An absorption refrigerating apparatus of the type using a motor driven medium circulator I and a heater for the boiler, a control for energizing the apparatus'including means associated with the apparatus responsive to a temperature rise resulting from the energizing of the apparatus and constructed to delay the operation of the motor driven circulator for a period after the energization of the apparatus.
16. An absorption refrigerating apparatus of the type using a motor-fan unit for circulating both the absorption solution between the boiler and absorber and a pressure equalizing medium between the evaporator and absorber and a heater for the boiler, a control for energizing the apparatus including means associated with the apparatus responsive to a temperature rise incident to the energizing of the apparatus and constructed to delay the operation of the motor fan unit for a period after the energization of the apparatus whereby the circulation of absorption I solution until the boiler has reached an operative temperature.
18. In an electric motor, a field structure, a rotor, means for energizing the field structure and means for retarding the rotation of the rotor, said means being constructed to release its retardation of the rotor after a predetermined interval.
19. The method of starting a rotary electric motor comprising energizing the motor field structure, delaying the rotation of the rotor and utilizing the energy supplied to the motor to govern the period of delay.
20. The method of starting a rotary electric motor comprising energizing the motor field structure, blocking the rotor by submerging it in a lubricant solid at ordinary temperatures but which fuses at higher temperatures and utilizes the energy supplied to the motor and the heat of fusion of the lubricant to predetermine the period the rotor remains blocked.
21. An absorption refrigerating apparatus comprising a boiler, a condenser, an evaporator and an absorber, conduits connected to said evaporator and absorber to form an inert gas circuit between said evaporator and absorber, said apparatus being charged with a refrigerant, a liquid absorbent and an inert gas, and power operated means in said closed circuit for circulating the inert gas in said circuit, said power operated means comprising a motor rotor and fan in which the motor rotor is submerged in a lubricant, and said power operated means being positioned in a part of said inert gas circuit inaccessible to the liquid medium within the apparatus under normal operating conditions.
22. An absorption refrigeratingapparatus comprising a boiler, an evaporator and an absorber, conduits connecting said evaporator and absorber to form an inert gas circuit therebetween, conduits connecting the boiler and absorber to form a solution circuit therebetween, said apparatus being charged with a refrigerant, a liquid absorbent and an inert gas, power operated means in said evaporator-absorber circuit for circulating an inert gas in'said circuit, said power operated means comprising a motor rotor and fan enclosed in a casing and in which the motor rotor is submerged in a lubricant, and a conduit leading from the discharge side of said fan to the boiler-absorber circuit and so related thereto as to circulate absorption solution in said circuit, said motor fan casing being positioned in a part of said evaporator-absorber circuit normally inaccessible to liquid mediums in the apparatus but subject to being flooded during idle periods, said conduit leading from the discharge side of the 7 fan to the boiler-absorber circuit being so related to the motor fan casing as to drain any liquid accumulated in the motor fan casing, to the boiler-absorber circuit.
23. An absorption refrigerating apparatus comprising a boiler, an evaporator and an absorber, conduits connecting said evaporator and absorber to form an inert gas circuit therebetween, said apparatus being charged with a refrigerant, a liquid absorbent and an inert gas, power operated means in said circuit between the evaporator and absorber for circulating the inert gas in its circuit, said power operated means comprising a motor fan unit in which the motor rotor is submerged in a lubricant and is positioned in a the evaporator and absorber that any accumulated liquid medium will drain away from the fan unit during idle periods whereby the lubricant in the motor housing will not be diluted by the liquid mediums within the system.
24. An absorption refrigerating apparatus of the type having a motor fan unit for circulating an inert medium in a circuit between the evaporator and absorber and which is also charged with liquid mediums, in which the motor ian unit positioned in a part of the circuit normally inaccessible to the liquid mediums in the apparatus but subject to being flooded with the liquid medium when the apparatus is tipped and in which the motor rotor is submerged in a lubricant which is solid at ordinary temperatures.
25. An absorption refrigerating apparatus in cluding a motor driven medium circulator, said motor driven medium circulator including a motor rotor submerged in a lubricant and said apparatus being charged with a refrigerant and a' solvent, said lubricant being indisplaceable by the refrigerant or the solvent.
26. An absorption refrigerating apparatus including a motor fan unit for circulating the mediums in the apparatus, said motor fan unit having the motor rotor submerged in a lubricant and said apparatus being charged with a refrigerant and a solvent therefor, said motor fan unit being positioned in a part of the apparatus normally inaccessible to the liquid mediums in the apparatus but subject to be flooded thereby when theapparatus is tipped, said lubricant being indisplaceable by the liquid mediums in the apparatus.
27. An absorption refrigerating apparatus comprising an inert gas circuit and a solution circuit, a motor circulator unit for circulating a medium in one of said circuits, said circulator unit including a rotor submerged in a solid lubricant.
28. An absorption refrigerating apparatus of the type having liquid and gaseous mediums therein and closed circuits for said mediums, in combination with a circulator unit for at least one 'of said mediums hermetically sealed within the walls of the apparatus, said circulator unit including a motor rotor and fan, said motor rotor being submerged in a lubricant and positioned outside said circuits.
29. An absorption refrigerating apparatus comprising an evaporator and an absorber, conduits connecting said evaporator and absorber to form an inert gas circuit therebetween, said apparatus being charged with a refrigerant, an absorbent,
circuit, saidpower operated means comprising a' motor fan rotor in which the motor rotor is submerged in a lubricant non-fluid at ordinary temperatures.
30. An absorption refrigerating apparatus of the type having a motor fan unit for circulating an inert medium in a circuit between the evaporator and absorber, said motor comprising a vertically extending casing having an upper fan casing and a lower shell, a motor rotor in said shell and a motor field outside said shell supporting it against internal pressure, said shell containing a. solid lubricant.
31. An absorption refrigerating apparatus including a heater for the boiler and a motor fan unit for circulating the mediums in the apparatus in which the motor fan rotor is submerged in the lubricant solid at ordinary temperatures but fusible at higher temperatures, said, lubricant having a heat of fusion of such value and being present in such amount relative to the heating rate of the boiler and the power input to the motor that the heat of the motor will fuse the lubricant by the time the heater has brought the boiler to operating temperatures when the heater and motor are simultaneously energized.
32. That improvement in the art of refrigeration which comprises lubricating the moving parts of a refrigerating apparatus by means of a lubricant which is non-fluid at ordinary temperatures and liquid at the operating temperature of the apparatus, whereby the lubricant cannot be displaced by the refrigerating medium during inoperative periods.
33. That improvement in the art of lubricating motors which comprises submerging the motor rotor in a lubricant which is non-fluid at ordinary temperatures but fluid at the operating temperature of the motor.
34. A fractional horse power motor fan unit for circulating an inert medium in an absorption refrigerating apparatus comprising a ver-- tically extending hermetically sealed casing and a motor fan rotor rotatably mounted in said casing, said motor rotor being submerged in a lubricant solid at ordinary temperatures but fusible at higher temperatures.
35. A fractional horse power motor fan unit for circulating an inert medium in an absorption refrigerating apparatus comprising a vertically extending hermetically sealed casing, a motor fan rotor rotatably mounted in said casing, and a field structure externally of said casing, said motor rotor being submerged in a lubrica'nt, said lubricant being of such nature that it fuses due to the heat generated by said field structure.
36. A motor comprising a casing and a rotor mounted in said casing, said casing containing a lubricant solid at ordinary temperatures but fusible at higher temperatures.
37. That improvement in the art of refrigeration in which a power driven circulator is used to circulate the medium which comprises, charging a refrigerating apparatus with a liquid working medium, charging a fused lubricant into the apparatus in a position to surround the moving parts of the circulator, allowing the lubricant to congeal and re-fusing the lubricant prior to operation whereby the lubricant cannot be displaced by the liquid working medium during shipment or other inoperative periods and is in a condition to lubricate the moving parts of the circulator during operation.
38. An absorption refrigerating apparatus of the type having liquid and gaseous mediums therein and closed circuits for said mediums, in combination with a circulator unit for at least one of said mediums, said circulator unit including a movable element located in a closed casing hermetically sealed to, in open communication with and extending from one of said circuits so as to be outside the path of flow of the medium being circulated in said circuit and a lubricant in said casing whereby the movable element will be lubricated and the lubricant will not be carried along by the circulating medium to other parts of the apparatus.
39. In an absorption refrigerating apparatus of the type having liquid and gaseous mediums therein and closed circuits for said mediums, in combination with a circulator unit for at least one of said mediums, said circulator unit including a movable element located in a closed casing hermetically sealed to, in open communication with and extending from one of said circuits so as to be outside the path of flow of the medium being circulated in said circuit and a lubricant in said casing having a specific gravity higher than the medium being circulated in said circuit whereby the movable element wll be lubricated and the lubricant will not be carried along with the circulating medium to other parts of the apparatus.
40. In combination, an absorption refrigerating apparatus including a closed inert gas circuit and means for circulating an inert gas in said circuit, said means including a movable element in a closed casing hermetically sealed to, in open communication with and extending from said circuit so as to be out of the path of flow of the inert gas in said circuit and said casing containing a lubricant whereby said movable element will be lubricated and the lubricant will not be entrained in the circulating inert gas and be carried to the other parts of the apparatus.
- CHARLES H. MACFARLAND.
US317389A 1940-02-05 1940-02-05 Refrigeration Expired - Lifetime US2271563A (en)

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GB13004/40A GB543315A (en) 1940-02-05 1940-08-14 Improvements in or relating to absorption refrigerating apparatus
FR869778D FR869778A (en) 1940-02-05 1941-02-05 Refrigeration process and refrigerator apparatus

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060228238A1 (en) * 2005-04-06 2006-10-12 Andrews Gregory C Coolant pump for x-ray device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060228238A1 (en) * 2005-04-06 2006-10-12 Andrews Gregory C Coolant pump for x-ray device

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